Energy efficient apparatus for removing emissions

ABSTRACT

Disclosed is an apparatus for removing emissions, originated in the manufacturing industry, especially from polymerization operations and thermoplastic polymer processing operations which has a plurality of ducts, an entrance for collecting air, containing the emissions and an exit for exiting exhaust air, a first heat exchanger which has a hot side with an entrance and an exit and a cold side with an entrance and an exit, a second heat exchanger, which has a hot side with an entrance and an exit and a cold side, a liquid removal system, and a fan, whereby the first heat exchanger is connected with the entrance of the hot side to the entrance of the duct system and with the exit of the hot side to the entrance of the hot side of the second heat exchanger by a duct; the exit of the hot side of the second heat exchanger is connected to the entrance of the cool side of the first heat exchanger by a duct; the precipitator is connected to the exit of the cool side of the first heat exchanger by a duct and to the fan by a duct, the fan is connected to the exit of the duct system.

FIELD OF THE INVENTION

The present invention relates generally to an apparatus for removing emissions which originate in various manufacturing industries, such as the chemical, pharmaceutical, coatings, recycling and oil industries. Especially, it relates to a process which is suitable for removing monomer, oligomer, additives and water emissions before, during and after the polymerization reaction for the manufacture of thermoplastic polymers and during thermoplastic polymer processing operations like extrusion, injection molding and fiber spinning operations.

BACKGROUND OF THE INVENTION

In the manufacturing industry, like the chemical, pharmaceutical, coating, recycling and oil industry, there exists a broad variety of sources for emissions which are released in the environment, which is not desirable. For example, in chemical reactions, emissions of reaction components, additives and solvents may be released. During coating of cars, vapors of coatings, additives and solvents may be released. During recycling of polymers, monomers or oligomers of the hydrolyzed polymer may be released. During cleaning of reactors, chemicals and solvents may be released.

Before, during and after the polymerization reaction for the manufacture of thermoplastic polymers like polyamides, polyester, polyolefins, polycarbonates, polystyrenes, polyacrylonitriles, polyurethanes, polysulfones, polyethersulfones, polyvinylchloride, copolymers and mixtures thereof, monomer vapors may be released in the environment from transportation tanks, storage tanks, pipelines, ducts, polymerization reactors, polymer melts, polymer strands, water bath, cutters, dryers and the like. During thermoplastic polymer processing like injection molding or extrusion, the thermoplastic polymers are for example extruded through an extruder into strands for chip production or into films, fibers, profiles, tubes and the like. During the extrusion at a temperature of from about 180° to about 350° C., monomer or oligomer vapors, compounds formed by thermal evaporation, thermal decomposition, or vapors of additives are released from the surface of the extruded polymers, which are leaving the nozzle of the extruder. These vapors evaporate immediately into an aerosol that would form deposits in the neighborhood of the extruder and therefore, must be removed, which is usually done by the quench air removal. The exhaust air is usually released in the environment, which is not desirable.

During the manufacture of synthetic yarns, a heat setting step is applied to the yarn for setting a twist in the yarn. In a heat setting unit, heat in form of hot air and/or steam is applied to the yarn. The air and/or steam contains emissions like monomers, oligomers and finish oils, when it exits the heat setting unit, which should be removed.

U.S. Pat. No. 4,676,807 discloses a process for removal of liquid aerosols from gaseous streams by passing the stream through a coalescing filter. In the examples of this patent, oil and water aerosols were tested.

U.S. Pat. No. 4,759,782 which is a C.I.P. of an application which issued as U.S. Pat. No. 4,676,807 described above, discloses the coalescing filter for removal of liquid aerosols from gaseous streams.

The technical bulletin Wringer®, Des Champs Laboratories Inc., Va., describes an apparatus for the dehumidification of air.

An object of the present invention was to provide an apparatus for removing emissions from a broad variety of emission sources.

Another object of the present invention was to provide an apparatus for removing of emissions from polymerization operations and thermoplastic polymer processing operations.

Another object was an apparatus for removing emissions from fiber spinning operations.

Another object was an apparatus for removing emissions from a heat setting operation for the manufacture of synthetic yarns.

Still another object was an apparatus for removing emissions from a heat setting operation for the manufacture of polycaprolactam yarns.

SUMMARY OF THE INVENTION

The objects of the present invention could be achieved with an apparatus for removing emissions, which comprises:

a) a duct system, comprising a plurality of ducts and having an entrance for collecting air, containing the emissions, and an exit for exiting exhaust air;

b) a heat exchanger, having a hot side with an entrance and an exit and a cold side with an entrance and an exit;

c) means for cooling the air;

d) means for removing liquid droplets from the air;

e) means for moving the air through the apparatus;

the heat exchanger being connected by the entrance of the hot side with the entrance of the duct system and by the exit of the hot side with the entrance of the means for cooling the air by a duct; the means for cooling the air being connected to the entrance of the cool side of the first heat exchanger by a duct; the means for removing liquid droplets from the air being connected to the exit of the cool side of the heat exchanger by a duct and being connected to the exit of the duct system; the means for moving the being connected to a duct of the duct system.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a flow chart of a polymerization operation and a thermoplastic processing operation.

FIG. 2 is a schematic view of an apparatus of the present invention for removing emissions from a heat setting unit for synthetic yarns with two heat exchangers and one liquid removal system located between the second and the first heat exchanger.

FIG. 3 is a schematic view of a modified apparatus of the present invention, wherein the liquid removal system is located between the first heat exchanger and the fan.

FIG. 4 is a schematic view of another modified apparatus of the present invention, which has two liquid removal systems.

FIG. 5 is a schematic view of the apparatus shown in FIG. 2, wherein a cooling tower is connected to the second heat exchanger.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

The apparatus of the present invention is suitable for removing emissions from a broad variety of emission sources in the manufacturing industry like the chemical, pharmaceutical, coating, recycling and oil industry. The following example from the chemical industry show the applicability of the process for removing emissions which are released before, during and after the polymerization reaction for the manufacture of polymers and during the thermoplastic processing of polymers into polymer articles.

Articles, made from thermoplastic polymers, like polyamides, polyesters, polyolefins, polycarbonate, polyacrylonitrile, polyurethane, polysulfons, polyethersulfones, polyvinylchloride and the like are manufactured in several steps. One step is the polymerization of monomers to a thermoplastic polymer, followed by the thermoplastic processing into the final shape of the article.

FIG. 1 shows a general flow chart for the manufacture of such articles including a polymerization operation comprising the feedstock transfer (1), the feedstock processing (2), the reactor (3) and the polymer processing (4) as well as a thermoplastic processing operation comprising the thermoplastic processing (5), conditioning (6) and the final thermoplastic polymer product (7). Also included in the operation is a cleaning operation (8) and a recycling operation (9).

The feedstock transfer (1) includes the monomer transport via pipeline, truck, rail, drum, sack and the like. The feedstock processing (2) comprises storage tanks, mixing and conditioning of monomers. The reactor (3) comprises the reaction chamber where the polymerization reaction takes place and all the peripheral equipment like columns and pipes. After the polymerization is finished the polymer melt exits the reactor and is transformed into chips, flakes or granules in the polymer processing (4) which comprises pump blocks where the polymer melt is formed into polymer strands, a water bath for cooling the polymer strands, a cutter for cutting the polymer strands into chips and a dryer to dry the chips. In fluidized bed reactors for the manufacture of for example polyolefins, the polymer is formed into granules, which exit the reactor without further polymer processing (4).

In the thermoplastic processing operation, the thermoplastic polymer is melted, for example, in an extruder or injection molding machine which is shown as thermoplastic processing (5). The polymer exits the injection molding machine in form of a shaped article. The polymer melt exits the extruder in form of strands, films, fibers, profiles, tubes and the like, which are conditioned in the conditioning (6), which includes the treatment with quench air, finish application, drawing, texturizing, heat setting and the like to form the final thermoplastic article (7). In all seven stages, emissions may be released in the environment like monomers, oligomers, additives like finish oils, solvents, decomposition products and the like. For example emissions of monomers may be released during feedstock transfer from pipelines, trucks, rails or drums from vents of storage tanks or reactors, during polymer processing, during thermoplastic processing from the exit of the extruder or injection molding machine, during conditioning of for example fibers with regard to quenching, finish application or heat setting.

Emissions may be released also in cleaning operations (8) of the equipment used in (1) to (7) and (9) and in recycling operations (9), where thermoplastic polymer is depolymerized in monomers, the monomers are recovered and again polymerized. The process of the present invention is applicable to all emission sources, originated in polymerization operations, thermoplastic processing operations, cleaning operations or recycling operations, especially multicomponent air streams containing caprolactam emissions, finish oils and water.

The following is a description of the apparatus of the present invention applied to heat setting of synthetic yarns as one example of the above mentioned multiplicity of possibilities for emissions.

One apparatus of the present invention for removal of emissions from heat setting of synthetic yarns is described with reference to FIG. 2.

FIG. 2 shows a heat setting operation for the heat setting of synthetic yarns and an apparatus for removing emissions originated in the heat setting operation. Twisted yarn (10) is heat set in the heating chamber (11) with hot air and/or steam, from duct (12), followed by winding up on a package (13). The hot air and/or steam, containing the emissions from the yarn (10), exits the heating chamber (11) over duct (14) and is directed to the first heat exchanger (15), where it is cooled and which has a hot side with an entrance (16) and an exit (17) and a cold side with an entrance (18) and an exit (19).

In the first heat exchanger (15) a part of the emissions condenses and is removed over pipes (20) and (21).

The cooled air exits the first heat exchanger (15) and is directed via duct (22) to the second heat exchanger (23), which has a hot side with an entrance (24) and an exit (25) and a cold side with an entrance (26) and an exit (27). The air is further cooled in this second heat exchanger (23) and condensibles are removed over pipes (28) and (21). The second heat exchanger is cooled with a cooling medium like air, water, an aqueous solution, an organic solvent, an inorganic solvent and the like. The air exiting the hot side of the second heat exchanger (23) at exit (25) is directed over duct (29) to the liquid removal system (30) for removing liquid droplets from the air. A suitable liquid removal system (30) is an electrostatic precipitator, a mist eliminator such as a demister pad, mesh pad, and the like, a fiberbed filter and combinations thereof. Preferred is an electrostatic precipitator, a mist elminator and a combination of a mist eliminator and an electrostatic precipitator, connected by a duct to each other. The term duct also includes connections of all kinds and/or shapes between two units for the transport of air and is not limited to tubes. Condensates in the liquid removal system (30) are removed over pipes (31).

The air, exiting the liquid removal system (30) is directed over duct (32) to the first heat exchanger (15), wherein it is heated by the incoming hot air from duct (14) through entrance (16), thereby cooling the incoming hot air. Condensibles are removed over pipes (23) and (17). The heated air, exiting the first heat exchanger (15) at exit (19) is directed over duct (33) to the exhaust duct (35) by the fan (34).

FIG. 3 shows a modification of the apparatus, shown in FIG. 2. In this modified apparatus, the liquid removal system (36) is located between the first heat exchanger (15) and the fan (34), so that the air exiting the cool side of the first heat exchanger (15) at the exit (19) is directed over duct (33) to the liquid removal system (36). A suitable liquid removal system (36) is an electrostatic precipitator, a mist eliminator such as a demister pad, a mesh pad and the like, a fiberbed filter and combinations thereof. Preferred is an electrostatic precipitator, a mist eliminator and a combination of a mist eliminator and an electrostatic precipitator, connected by a duct to each other. Precipitates in the liquid removal system (36) are removed over pipe (37) and (21).

The air exiting the liquid removal system (36) is directed over duct (38) to the exhaust duct (35) by the fan (34). The remaining parts of the apparatus are identical to the apparatus shown in FIG. 2.

FIG. 4 shows a combination of the apparatus shown in FIG. 2 and FIG. 3, having two liquid removal systems (30) and (36), the parts thereof are described above.

FIG. 5. shows a modification of the apparatus, shown in FIG. 4, which includes a cooling tower (39) for cooling the water for the cold side of the second heat exchanger (23). Cooled water from the cooling tower (39) is directed over pipe (40) to the entrance (26) of the cold side of the second heat exchanger (23), where it cools the incoming hot air from duct (22) which enters the second heat exchanger (23) at entrance (24) and is thereby heated. The heated water exits the second heat exchanger (23) at exit (27) and is recirculated through pipe (41) to the cooling tower (39). The remaining parts are identical to the apparatus shown in FIG. 4 and described in FIG. 2 and FIG. 3.

The apparatus of the present invention is applicable to the polymerization and thermoplastic processing of all thermoplastic polymers, especially polyamides, polyesters, polyolefins, polycarbonates, polystyrenes, polyacrylonitriles, polyurethanes, polysulfones, polyethersulfones, polyvinylchloride, copolymers and mixtures thereof.

For the manufacture of fibers all fiber forming thermoplastic materials are suitable, especially polyamides, polyesters, polyolefins, polycarbonate and polyacrylonitrile.

Suitable polyamides are nylon 6, nylon 6/6, nylon 6/9, nylon 6/10, nylon 6/12, nylon 11, nylon 12, copolymers thereof and mixtures thereof. Preferred polyamides are nylon 6 and nylon 6/6. A suitable polyester is polyethylene terephthalate.

For the manufacture of fibers, the polymer is fed into an extruder in form of chips or granules, or as molten resin, melted and directed via jacketed Dowtherm® (Dow Chemical, Midland, Mich.) heated polymer distribution lines to the spinning head. The polymer melt is then metered by a high efficiency gear pump to spin pack assembly and extruded through a spinnerette. The fibers are spun at a temperature of from about 180° to 350° C. according to the respective polymer with a spinning speed of from about 1000 to about 5000 m/min, dependant on the type of polymer.

In the heatsetting process the yarn is placed on a conveying belt (not shown in the Fig.'s) and sent through the heating chamber (11) in which hot air with or without steam is circulated around the yarn. This process sets the twist in the yarn, as well as improving its dyeability. During this process, emissions like monomers and/or oligomers and/or finish oil are released. In the case of polycaprolactam, caprolactam and finish oil is released.

In the operation of the apparatus of the present invention which is described with reference to FIG. 2, air, containing the emissions, is collected at the exit of the heating chamber (11) in a duct system, which has a plurality of ducts, an entrance for collecting air, containing the emissions and an exit for exiting exhaust air. The air in duct (14) has a temperature of from about 40° to about 300° C., preferably from about 45° to about 170° C. The air, containing the emissions, is directed through duct (14) to the hot side of the heat exchanger, where it is cooled to a temperature of from about 21° to about 90° C. preferably from about 32° to about 71° C. Condensation occurs in this heat exchanger and the condensate is removed over ducts (20) and (21). A suitable heat exchanger for cooling the air coming out of duct (14) is the Wringer® unit from Des Champs Laboratories, Va. The air exiting the first heat exchanger is directed to the means for cooling the air, where it is further cooled to about 0.1° to about 65° C., preferably to about 4° to about 54° C. Suitable means for cooling the air are cooler, heat exchanger and the like. If a second heat exchanger (23) is used as a means for cooling the air, it is cooled with a cooling medium like air, water, an aqueous solution, an organic solvent, an inorganic solvent and the like. The heat transferred to the cooling medium can be rejected by a cooling tower or another heat exchanger. Suitable heat exchangers are air to air counterflow eat exchangers like the Z-Duct® Series 84-1000 from Des Champs Laboratories, Va. or coil heat exchanger from Marlo Coil with a cooling tower and water as a cooling medium.

The cooled air exiting the means for cooling the air is directed to the means for removing the liquid droplets from the air. A suitable means for removing liquid droplets is the liquid removal system (30). Suitable liquid removal systems are electrostatic precipitators like those from United Air Specialists, Trion, and Beltran; mist eliminators like mesh filters such as Permanent Heavy Duty Air or Grease Filters by Rutzler; and fiberbed filters like those from KOCH, and combinations thereof. Preferred are an electrostatic precipitator, a mist eliminator and a combination of a mist eliminator and an electrostatic precipitator being connected by a duct to each other.

The air leaving the means for removing liquid droplets from the air is directed to the cool side of the heat exchanger, where it is heated by the incoming hot air from duct (14) to a temperature of from about 4° to about 93° C., preferably to a temperature of from about 10° to 77° C. The heated air exiting the cool side of the heat exchanger is directed over duct (33) to the exhaust duct (35) by the means for moving the air through the apparatus and released in the environment. A suitable means for moving the air through the apparatus is a fan.

The opacity is reduced from greater than 25% entering the system unit at duct (14) to less than 5% exiting the system at duct (26). The exhaust air is estimated to have less than 20% by volume of caprolactam emissions and less than 20% by volume of finish oil emissions.

EXAMPLE 1

Nylon 6 carpet yarn (Ultramid® B of BASF AG, Germany, with a relative viscosity of 2.5, measured as a 1% by weight solution in 90% formic acid. at 25° C.) was heat set in two heat setting units from Suessen.

The combined through put of fiber was 284 kg/hr. Steam injected into each heatsetting unit at a rate of 483 kg/hr.

The air containing the emissions at the exit of the heating chamber had a flow rate of 67 m³ /min. a temperature of 103° C. dry bulb and 72° C. wet bulb, and consisted of air, water vapor, caprolactam, and finish oil. This air stream was cooled in the first heat exchanger, which was a Wringer unit manufactured by Des Champes Laboratories consisting of an air-to-air Z-Duct®, Series 84-1000 heat exchanger followed by an air-to-water heat exchanger, with Marlo cooling coils. The air stream leaving the Suessen heatsetting heatsettng units was cooled to saturation by the first air-to-air heat exchanger to 72° C. dry and wet bulb. The air leaving the first heat exchanger was further cooled by a second heat exchanger., an air-to-water heat exchanger containing Marlo cooling coils, with 0.5 m³ /min and 25.6° C. cooling tower water from an Amcot cooling tower to an air temperature of 43° C. dry and wet bulb. Approximately 0.02 m³ /min. condensate was formed from both heat exchangers. The air was directed a mesh-type Permanent Heavy Duty Air or Grease Filter mist eliminator by Rutzler. The air leaving the mist eliminator was directed to the first air-to-air heat exchanger to serve as the cooling medium for the air stream leaving the Suessens. The first heat exchanger also served as a medium for heating the air leaving the mist eliminator to an exit temperature of 66° C. dry bulb and 42° C. wet bulb before entering the electrostatic precipitator by Thiel Industries. The air exiting the electrostatic precipitator was then exhausted by a fan to the exhaust duct. 

We claim:
 1. Apparatus for removing fiber finish oil emissions entrained in a moisture-laden air stream obtained from a synthetic fiber processing system and for reducing opacity of the air stream so that the air stream may be exhausted to atmosphere, said apparatus comprising:(a) an air collection duct system for collecting the fiber finish oil emissions-containing moisture-laden air stream; (b) a cooling system which includes first and second heat exchangers fluid-connected in series with one another and connected operatively to said air collection duct system, said cooling system for receiving said fiber finish oil emissions-containing moisture-laden air stream and bringing said air stream into heat exchange relationship with a heat-exchange fluid so as to cool the air stream to a moisture saturation temperature at which moisture contained in the air stream condenses to liquid so as to form a first aqueous liquid condensate stream, and an air discharge stream which is discharged from said second heat exchanger and contains moisture-saturated air and liquid droplets of said fiber finish oil emissions; and (c) a liquid removal system for receiving said air discharge stream and removing said liquid droplets of said fiber finish oil emissions therefrom to form a second aqueous liquid condensate stream containing a substantial portion of said fiber finish oil emissions; wherein (d) said air discharge stream is fluid-connected to said first heat exchanger so as to serve as said heat-exchange fluid in heat-exchange relationship with said fiber finish oil emissions-containing moisture-laden air stream such that heat transferred to said air discharge stream from said fiber finish oil emissions-containing moisture-laden air stream causes said sir discharge stream to be heated to an extent to cause desaturation of the air discharge stream and thereby form an exhaust air stream having reduced opacity which may be released to atmosphere.
 2. The apparatus according to claim 1, which includes air moving means for moving the air stream through the apparatus, said air moving means being connected to said first heat exchanger in said exhaust air stream.
 3. The apparatus according to claim 2, wherein the liquid removal system is an electrostatic precipitator.
 4. The apparatus according to claim 2, wherein the liquid removal system includes both a mist eliminator and an electrostatic precipitator.
 5. The apparatus according to claim 2, wherein the air moving means is a fan.
 6. The apparatus according to claim 1 or 2, wherein the liquid removal system is fluid-connected within said air discharge stream at a location between said second heat exchanger and said first heat exchanger.
 7. The apparatus according to claim 6, wherein the liquid removal system includes at least one liquid removal unit selected from the group consisting of an electrostatic precipitator, a mist eliminator, and a fiberbed filter.
 8. The apparatus according to claim 1 or 2, wherein said liquid removal system includes first and second liquid removal units for removing liquid droplets from the air.
 9. The apparatus according to claim 8, wherein each of said first and second liquid removal units of said liquid removal system is selected from the group consisting of an electrostatic precipitator, a mist eliminator, and a fiberbed filter.
 10. The apparatus according to claim 8, wherein one of said first and second liquid removal units of the liquid removal system is an electrostatic precipitator.
 11. Apparatus according to claim 8, wherein one of said first and second liquid removal units of the liquid removal system includes a mist eliminator and another of said first and second liquid removal units of the liquid removal system is an electrostatic precipitator.
 12. The apparatus according to claim 1, wherein the liquid removal system includes at least one liquid removal unit selected from the group consisting of an electrostatic precipitator, a mist eliminator, and a fiberbed filter.
 13. The apparatus according to claim 1, wherein the liquid removal system is an electrostatic precipitator.
 14. The apparatus according to claim 1, wherein the liquid removal system includes both a mist eliminator and an electrostatic precipitator.
 15. The apparatus according to claim 1, wherein the second heat exchanger brings said air stream into heat-exchange relationship with a cooling medium selected from the group consisting of water, an aqueous cooling solution, an organic solvent, an inorganic solvent, and mixtures thereof.
 16. The apparatus according to claim 15, wherein the cooling medium of the second heat exchanger is water.
 17. The apparatus according to claim 17, further comprising a cooling tower for cooling the water cooling medium, said cooling tower being fluid connected to said second heat exchanger so as to bring said water cooling medium into heat-exchange relationship with said air stream.
 18. In a heat-setting apparatus for heat-setting twisted nylon carpet yarn which includes a heat-setting chamber for subjecting the nylon carpet yarn to a heated moisture-laden air environment at a temperature between about 40° to about 300° C. to thereby heat-set the same, the improvement comprising a system for reducing condensable vaporous caprolactam and finish oil emissions contained within an air stream removed from said heated air environment of the heat-setting chamber during heat-setting of said twisted nylon carpet yarn, and for reducing opacity of said emissions-containing air stream sufficient to exhaust said air stream to .atmosphere, said system comprising:(a) first and second heat exchangers fluid-connected to one another in series, said first heat exchanger receiving the moisture-laden air containing condensable vaporous caprolactam and finish oil emissions removed from said heated air environment of said heat-setting chamber and bringing the air stream into heat-exchange relationship with a first heat-exchange fluid which cools the air stream to a temperature between about 21° to about 90° C., and said second heat exchanger receiving the air stream from said first heat exchanger and bringing the air stream into heat-exchange relationship with a second heat-exchange fluid to further cool the air stream to a temperature between about 0.1° to about 65° C., said first and second heat exchangers thereby cooling the air stream to a moisture saturation temperature sufficient to form a liquid aqueous condensate stream containing a condensed portion of said emissions, and an air discharge stream in which a remaining portion of said emissions in the form of liquid droplets is entrained; and (b) an electrostatic precipitator for removing said liquid droplets from said air discharge stream and thereby remove a substantial part of said remaining portion of said emissions entrained therein; and wherein (c) the air discharge stream from said second heat exchanger is recycled to said first heat exchanger as said first heat-exchange fluid so that the moisture-laden air containing condensable vaporous caprolactam and finish oil emissions removed from said heated air environment of said heat-setting chamber heats the air discharge stream to a temperature above its saturation temperature of between about 4° to about 93° C. sufficient to desaturate the air discharge stream of moisture and thereby form an exhaust air stream having a reduced opacity of less than 5% which may be released to atmosphere
 19. In the heat setting apparatus of claim 18, the improvement wherein said electrostatic precipitator is fluid-connected to and between said first and second heat exchangers in the recycle of said air discharge stream from said second heat exchanger to said first heat exchanger.
 20. In the heat setting apparatus of claim 18, the improvement wherein said electrostatic precipitator is fluid-connected to and downstream of said first heat exchanger in the air discharge stream.
 21. In the heat setting apparatus of claim 18, the improvement further comprising a mist eliminator which is disposed in said air discharge stream in series with said electrostatic precipitator.
 22. In the heat setting apparatus of claim 21, the improvement wherein said mist eliminator is fluid-connected to said electrostatic precipitator upstream of said electrostatic: precipitator.
 23. In the heat setting apparatus of claim 21, the improvement wherein said mist eliminator is fluid-connected to said electrostatic precipitator downstream of said electrostatic precipitator.
 24. In the heat setting apparatus as in any one of claims 18-23, the improvement further comprising a cooling tower fluid-connected to said second heat-exchanger, said cooling tower for cooling said second heat exchange fluid discharged from said second heat exchanger, and supplying the cooled second heat exchange fluid to said second heat exchanger.
 25. In the heat setting apparatus of claim 24, the improvement wherein said second heat exchange fluid is water. 